WO2021193144A1 - Method for producing bonding composition - Google Patents

Method for producing bonding composition Download PDF

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Publication number
WO2021193144A1
WO2021193144A1 PCT/JP2021/010064 JP2021010064W WO2021193144A1 WO 2021193144 A1 WO2021193144 A1 WO 2021193144A1 JP 2021010064 W JP2021010064 W JP 2021010064W WO 2021193144 A1 WO2021193144 A1 WO 2021193144A1
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Prior art keywords
liquid medium
copper particles
copper
dispersion
bonding composition
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PCT/JP2021/010064
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French (fr)
Japanese (ja)
Inventor
圭 穴井
真一 山内
亭來 趙
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三井金属鉱業株式会社
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Application filed by 三井金属鉱業株式会社 filed Critical 三井金属鉱業株式会社
Priority to EP21776056.0A priority Critical patent/EP4129529A4/en
Priority to US17/910,925 priority patent/US20230137716A1/en
Priority to CN202180021804.8A priority patent/CN115297978A/en
Priority to JP2022509926A priority patent/JPWO2021193144A1/ja
Priority to KR1020227029944A priority patent/KR20220154679A/en
Publication of WO2021193144A1 publication Critical patent/WO2021193144A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00Making metallic powder or suspensions thereof
    • B22F9/16Making metallic powder or suspensions thereof using chemical processes
    • B22F9/18Making metallic powder or suspensions thereof using chemical processes with reduction of metal compounds
    • B22F9/24Making metallic powder or suspensions thereof using chemical processes with reduction of metal compounds starting from liquid metal compounds, e.g. solutions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F7/00Manufacture of composite layers, workpieces, or articles, comprising metallic powder, by sintering the powder, with or without compacting wherein at least one part is obtained by sintering or compression
    • B22F7/06Manufacture of composite layers, workpieces, or articles, comprising metallic powder, by sintering the powder, with or without compacting wherein at least one part is obtained by sintering or compression of composite workpieces or articles from parts, e.g. to form tipped tools
    • B22F7/062Manufacture of composite layers, workpieces, or articles, comprising metallic powder, by sintering the powder, with or without compacting wherein at least one part is obtained by sintering or compression of composite workpieces or articles from parts, e.g. to form tipped tools involving the connection or repairing of preformed parts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F1/00Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F1/00Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
    • B22F1/05Metallic powder characterised by the size or surface area of the particles
    • B22F1/054Nanosized particles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F1/00Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
    • B22F1/05Metallic powder characterised by the size or surface area of the particles
    • B22F1/054Nanosized particles
    • B22F1/0545Dispersions or suspensions of nanosized particles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F1/00Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
    • B22F1/05Metallic powder characterised by the size or surface area of the particles
    • B22F1/054Nanosized particles
    • B22F1/056Submicron particles having a size above 100 nm up to 300 nm
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F1/00Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
    • B22F1/10Metallic powder containing lubricating or binding agents; Metallic powder containing organic material
    • B22F1/107Metallic powder containing lubricating or binding agents; Metallic powder containing organic material containing organic material comprising solvents, e.g. for slip casting
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C1/00Making non-ferrous alloys
    • C22C1/04Making non-ferrous alloys by powder metallurgy
    • C22C1/0425Copper-based alloys
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01BCABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
    • H01B1/00Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
    • H01B1/02Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors mainly consisting of metals or alloys
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01BCABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
    • H01B13/00Apparatus or processes specially adapted for manufacturing conductors or cables
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F2301/00Metallic composition of the powder or its coating
    • B22F2301/10Copper
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F2304/00Physical aspects of the powder
    • B22F2304/05Submicron size particles
    • B22F2304/056Particle size above 100 nm up to 300 nm
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F2998/00Supplementary information concerning processes or compositions relating to powder metallurgy
    • B22F2998/10Processes characterised by the sequence of their steps
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F2999/00Aspects linked to processes or compositions used in powder metallurgy
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F7/00Manufacture of composite layers, workpieces, or articles, comprising metallic powder, by sintering the powder, with or without compacting wherein at least one part is obtained by sintering or compression
    • B22F7/06Manufacture of composite layers, workpieces, or articles, comprising metallic powder, by sintering the powder, with or without compacting wherein at least one part is obtained by sintering or compression of composite workpieces or articles from parts, e.g. to form tipped tools
    • B22F7/08Manufacture of composite layers, workpieces, or articles, comprising metallic powder, by sintering the powder, with or without compacting wherein at least one part is obtained by sintering or compression of composite workpieces or articles from parts, e.g. to form tipped tools with one or more parts not made from powder

Definitions

  • the present invention relates to a method for producing a bonding composition.
  • Patent Document 1 includes a step of precipitating a metal powder by a wet reduction method and a step of adding a water-soluble organic solvent to the metal powder in a state where water is attached and replacing the water with the water-soluble organic solvent.
  • a method for producing a conductive paste is disclosed.
  • Patent Document 2 discloses a method for producing a metal powder for a conductive paste, in which the metal powder is washed with water or an organic solvent together with crushing. It is also disclosed in each of the above-mentioned patent documents that the dispersibility of the metal powder can be improved.
  • Patent Document 3 discloses a method for producing a silver-containing powder in which a dispersion liquid of silver-containing particles and a surfactant is vacuum freeze-dried.
  • Patent Document 4 discloses a silver powder obtained by converting silver particles obtained by a wet reduction method into a wet cake having a predetermined water content and crushing the wet cake by adding a dispersant. .. Similar to Patent Documents 1 and 2, these patent documents also disclose that the dispersibility of the metal powder can be improved.
  • Patent Documents 1 to 4 All of the techniques described in Patent Documents 1 to 4 have investigated the dispersibility of metal particles, but when the obtained metal powder or a conductive paste containing the metal powder is used for sintering, No studies have been made on the adhesion to other members.
  • the present invention is to provide a method for producing a bonding composition having excellent adhesion to other members at the time of sintering.
  • copper particles are generated in the first liquid medium by a wet reduction method to prepare a dispersion of the copper particles, and then, after that, While maintaining the wet state of the dispersion, the first liquid medium of the dispersion is finally replaced with the second liquid medium to obtain a bonding composition containing the copper particles and the second liquid medium. It provides a method for producing a bonding composition.
  • 1 (a) and 1 (b) are ultrasonic images of a sintered body obtained by firing the bonding compositions of Examples and Comparative Examples together with an object to be bonded.
  • the method of the present invention relates to the production of a bonding composition containing copper particles and a second liquid medium.
  • the bonding composition is suitably used, for example, as a conductive paste or a conductive ink for bonding two objects to be bonded to each other.
  • the bonding composition is preferably a dispersion containing copper particles as a conductive filler and a second liquid medium.
  • the production method of the present invention includes a step of producing copper particles in the first liquid medium by a wet reduction method to prepare a dispersion of copper particles, and a first step of the dispersion while maintaining a wet state of the dispersion. It is roughly divided into two steps, the step of finally replacing the liquid medium with the second liquid medium.
  • the "wet state” as used herein means a state in which the copper particles are not dried by, for example, heat treatment, and the surface of the copper particles is wet so that the vapor phase and the copper particles do not come into direct contact with each other. Specifically, it refers to a state in which the solid content concentration of the liquid medium dispersion of copper particles is maintained at 95% by mass or less.
  • finally replacing the first liquid medium with the second liquid medium means that the first liquid medium is directly replaced with the second liquid medium, and the dispersion containing the second liquid medium, which is the final object, is contained. And, the first liquid medium is replaced with one or more other liquid media (excluding the first liquid medium and the second liquid medium) other than the second liquid medium, and the final liquid medium replacement In both aspects, in the step, another liquid medium (excluding the first liquid medium and the second liquid medium) is replaced with the second liquid medium to obtain a dispersion containing the second liquid medium which is the final target product. Including.
  • copper particles are generated in the liquid medium by the wet reduction method.
  • the wet reduction method is intended, for example, by mixing a copper compound as a copper source and a reducing compound in a first liquid medium to prepare a reaction solution, and reducing the copper compound in the reaction solution. Obtain copper particles.
  • the particle size of the particles can be easily controlled, and spherical particles can be easily obtained.
  • Copper particles can also be produced, for example, by the method described in Japanese Patent Application Laid-Open No. 2015-168878.
  • a solid copper compound and a solid reducing compound may be added at the same time to prepare a reaction solution. Further, at least one of the copper compound and the reducing compound may be dispersed or dissolved in the liquid medium in advance, and then one may be added to the other to prepare a reaction solution. When one of the copper compound and the reducing compound is added to the other, it may be added all at once, or may be added continuously or intermittently by a method such as dropping.
  • the copper compound it is preferable to use a compound that dissolves in a liquid medium.
  • a copper compound include water-soluble copper (II) salts such as copper chloride, copper acetate and copper sulfate. These copper compounds may be anhydrous or hydrated. These copper compounds can be used alone or in combination of two or more.
  • the copper compound is preferably 0.001 mol / L or more and 1 mol / L or less, and more preferably 0.1 mol / L or more and 0.5 mol / L or less in terms of the content of the copper element in the reaction solution. Mix. By setting the content of such a copper compound, copper particles having a small particle size can be obtained with high productivity.
  • the reducing compound reduces the copper ions of the copper source.
  • the reducing compound include hydrazine compounds such as hydrazine, hydrazine hydrochloride, hydrazine sulfate and hydrous hydrazine, sodium hydride, sodium sulfite, sodium hydrogen sulfite, sodium thiosulfate, sodium nitrite, sodium hyponitrite, and the like.
  • phosphite, sodium phosphite, hypophosphite, and sodium hypophosphite may be anhydrous or hydrated. These reducing compounds may be used alone or in combination of two or more.
  • hydrazine is particularly preferably used because it causes less impurities to be generated after reduction and less impurities are mixed into the obtained copper particles. From the viewpoint of strong reducing power and suppressing contamination of particles with impurities, it is more preferable to use only hydrazine anhydride or hydrate as the reducing compound.
  • the content of the reducing compound in the reaction solution is preferably 0.5 mol or more and 50 mol or less, more preferably 1 mol or more and 10 mol or less, and further preferably 2 mol or more and 5 mol or less with respect to 1 mol of the copper element.
  • the reduction of the copper compound by the reducing compound may be carried out only once, or may be carried out a plurality of times as necessary.
  • the content of the reducing compound described above is a value in terms of anhydride.
  • the reaction conditions of the reaction solution may be the reaction without heating from the start of mixing to the end of the reaction, or the reaction may be carried out under heating conditions. Further, from the viewpoint of uniformly generating the reduction reaction and obtaining copper particles having little variation in particle size, it is also preferable to continue stirring the reaction solution for the entire time from the start of mixing to the end of the reaction.
  • the reaction it is preferable to carry out the reaction so as to maintain 0 ° C. or higher and 80 ° C. or lower from the start time of mixing to the end time of the reaction.
  • the time from the start of mixing to the end of the reaction can be appropriately changed depending on the particle size of the target copper particles, but is preferably 0.5 hours or more and 4 hours or less, and more preferably 1 hour or more and 3 hours or less. be able to.
  • the above-mentioned time is the total of the time from the start time of each mixing to the end time of the reaction.
  • Copper particles are generated through the above steps. Since the copper particles are obtained by the wet reduction method, they are in the state of a dispersion of copper particles dispersed in the first liquid medium which is the liquid medium of the reaction liquid.
  • the generated copper particles are preferably 100 nm or more and 300 nm or less, more preferably 100 nm, represented by the volume cumulative particle size DSEM50 at a cumulative volume of 50% by volume measured by image analysis of scanning electron microscope observation. It is 250 nm or more and 250 nm or less. Since D SEM50 indicates the particle size of the primary particle, which is an object recognized as the smallest unit as a particle, judging from the geometrical shape on the outer shape, the copper particle is defined as such a particle size range. As a result, the bonding composition exhibits good packing properties and sinterability, is capable of exhibiting high adhesion to other members such as the object to be bonded, and is advantageous in forming a thin coating film. ..
  • the particle size of the copper particles can be appropriately adjusted, for example, by adjusting the molar ratio of the copper compound and the reducing compound, or by adjusting the time of the reduction reaction.
  • D SEM50 can be measured by, for example, the following method. First, using Mac-View, a software manufactured by Mountech, the image data of copper particles obtained by observing from directly above with a scanning electron microscope was read, and then 50 or more copper particles on the data were randomly selected. Then, the particle size (Haywood diameter) of the particles is measured. Next, from the obtained Haywood diameter, the volume when the particles are assumed to be true spheres is calculated, and the volume cumulative particle diameter at 50% by volume of the cumulative volume of the volume is defined as DSEM50 .
  • Mac-View a software manufactured by Mountech
  • the first liquid medium of the dispersion is replaced with the second liquid medium while maintaining the wet state of the copper particle dispersion.
  • the first liquid medium in the dispersion is finally contained in the bonding composition while maintaining the wet state of the dispersion.
  • One of the features is to replace it with a second liquid medium.
  • a bonding composition such as a conductive paste containing copper particles or a conductive ink as a conductive filler
  • dried copper powder obtained by drying the obtained copper particles is typically used.
  • the content of copper particles can be appropriately increased or decreased to easily prepare a paste or ink having a desired filler concentration.
  • the redispersion process becomes complicated because the copper particles in the dried copper powder are agglomerated or easily agglomerated. In some cases, redispersion itself became impossible. As a result, the coating film obtained by applying the bonding composition is difficult to be smooth and has poor adhesion to other members.
  • the surface of the copper particles may be altered by oxidation or the like during drying, and desired properties such as adhesion and conductivity may not be exhibited.
  • desired properties such as adhesion and conductivity may not be exhibited.
  • copper particles having a particle size suitable for ink or paste are used in a dry state, the complexity of redispersion and the deterioration of the particles due to oxidation and the like are remarkable.
  • the copper particles obtained are not dried and are subjected to the subsequent steps while being maintained in a wet state, so that the copper particles come into contact with oxygen in the atmosphere. It will be reduced. Further, by increasing the dispersibility of the copper particles when preparing the bonding composition, excessive stress generation during film formation and sintering is suppressed. As a result, it has been found that the bonding composition of the present invention can exhibit excellent adhesion to other members during sintering and can suppress peeling from other members due to excessive volume shrinkage during sintering. rice field.
  • Substitution of the first liquid medium to the second liquid medium may be performed directly (hereinafter, this is also referred to as “direct replacement"), and the first liquid medium to another liquid medium (however, the second liquid medium is excluded). ) May be replaced one or more times, and then finally replaced with a second liquid medium (hereinafter, this is also referred to as "indirect replacement").
  • the dispersions maintained in a wet state can be independently, for example, in the form of a slurry or a wet cake.
  • the method for replacing the liquid medium is not particularly limited as long as the wet state of the dispersion can be maintained regardless of direct substitution or indirect substitution.
  • repulp washing, decantation method, rotary filter method, filtration and the like are adopted. be able to.
  • the liquid medium may be replaced only once, or may be performed a plurality of times as needed.
  • the liquid medium is replaced by setting the temperature of the liquid medium to preferably less than 100 ° C., more preferably 80 ° C. or lower, and further preferably 60 ° C. or lower.
  • the temperature of the liquid medium is set to preferably less than 100 ° C., more preferably 80 ° C. or lower, and further preferably 60 ° C. or lower.
  • the components derived from the first liquid medium that can cause impurities are efficiently removed, and the second liquid contained in the target bonding composition.
  • the first liquid medium contained in the copper particle dispersion obtained by the wet reduction method is excluded from other liquid media (however, the first liquid medium and the second liquid medium are excluded. ) Is replaced at least once, and a second liquid medium is preferably used for the final replacement. That is, it is preferable to adopt indirect substitution as the present production method.
  • the first liquid medium is replaced with another liquid medium (however, the second liquid medium is excluded) multiple times, similarly, the first liquid medium is replaced with the first other liquid medium, and other liquid mediums are replaced.
  • the dispersion is replaced while maintaining a wet state. Is preferable.
  • the solid content concentration in each replacement step may be the same or different.
  • the first liquid medium dispersion of copper particles obtained by the wet reduction method is used as another liquid medium such as water.
  • the cleaning treatment for example, repulp cleaning, decantation method, rotary filter method, filtration and the like can be adopted as the method.
  • the cleaning treatment it is preferable that the copper particles after cleaning are subjected to the subsequent steps in the state of a dispersion that maintains a wet state.
  • the cleaning conditions at this time are, for example, when water is used as another liquid medium, the cleaning temperature is preferably less than 100 ° C, more preferably 15 ° C or more and 30 ° C or less. By carrying out under such conditions, it is possible to reduce impurities contained in the copper particles and to use the particles in the subsequent steps while keeping the particles uniformly dispersed. Then, the liquid medium dispersion of the washed copper particles is finally replaced with the second liquid medium while maintaining the wet state.
  • the method described in Examples described later can be mentioned, but as long as the effect of the present invention is exhibited, the method is described. It can be applied without particular limitation on the number of replacements and the type of liquid medium used. Then, the liquid medium dispersion of the copper particles is finally replaced with the second liquid medium while maintaining the wet state.
  • a bonding composition containing copper particles and a second liquid medium can be obtained.
  • the dispersion treatment of copper particles when preparing a bonding composition is simplified, and the agglutination of copper particles is reduced, so that a highly smooth coating film can be efficiently formed. Become. Moreover, the deterioration of the surface of the copper particles can be reduced.
  • the coating film formed by the bonding composition is sintered, the meltability of the copper particles is increased, the meltability of the copper particles is increased, and the contact area between the melted particles and other members is increased. Can be increased. As a result, it is possible to obtain a sintered body that is less likely to crack or peel and has excellent adhesion to other members.
  • the first liquid medium used in this production method one or more of water, alcohol, ketone, ester and ether is preferable from the viewpoint of efficiently advancing the reduction of copper by the wet reduction method, and the copper particles by the wet reduction method are used. From the viewpoint of increasing the compatibility with the copper salt and increasing the production efficiency of copper particles, one or more of water and alcohol are more preferable.
  • the second liquid medium used in this production method water, alcohol, ketone, ester, ether can be used as it is as a conductive paste or conductive ink from the viewpoint of increasing productivity. And one or more of hydrocarbons are preferable, and alcohol and hydrocarbons are more preferable.
  • the above-mentioned first liquid medium and second liquid medium may be the same as each other or may be different from each other.
  • another liquid medium (excluding the first liquid medium and the second liquid medium) from the viewpoint of achieving both a reduction in the residual amount of the first liquid medium and the ease of replacement with the second liquid medium, when using another liquid medium.
  • the other liquid medium it is preferable to use one or more of water, alcohol, ketone, ester, ether and hydrocarbon, and it is more preferable to use one or more of water and alcohol.
  • Examples of the alcohol include monohydric alcohols such as methanol, ethanol, n-propanol, 2-propanol and n-butanol, ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, butylene glycol and pentylene.
  • Monohydric alcohols such as methanol, ethanol, n-propanol, 2-propanol and n-butanol, ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, butylene glycol and pentylene.
  • Polyhydric alcohols such as diols such as glycol and hexylene glycol, triols such as glycerin, and polyols such as polyethylene glycol and polypropylene glycol can be used.
  • ester examples include the fatty acid ester of the polyhydric alcohol described above.
  • the fatty acid is, for example, a monovalent fatty acid having a carbon atom number of preferably 1 or more and 8 or less, and more preferably 1 or more and 5 or less.
  • the ester of the polyhydric alcohol preferably has at least one hydroxyl group.
  • ketone a ketone having an alkyl group bonded to a carbonyl group having 1 or more and 6 or less carbon atoms, particularly 1 or more and 4 or less is preferable.
  • Specific examples of the ketone include methyl ethyl ketone, acetone and the like.
  • ether examples include chain ethers such as dimethyl ether, ethyl methyl ether and diethyl ether, and cyclic ethers such as octacene, tetrahydrofuran and tetrahydropyran.
  • hydrocarbons examples include aliphatic hydrocarbons such as hexane, heptane, octane, nonane, decane, undecane, dodecane, tridecane, tetradecane, pentadecane, and hexadecane.
  • the first liquid medium and the second liquid medium to be used are compatible with each other under the conditions of 1 atm and 25 ° C.
  • Compatibility means a phenomenon in which two or more kinds of liquid components are mixed with each other to form a single phase in a fluid containing two or more kinds of liquid components.
  • the first liquid medium when the first liquid medium is replaced with another liquid medium one or more times, or when the first liquid medium, the first other liquid medium, or another liquid medium is used for replacement twice or more.
  • the other liquid media that are continuous in the process and the combination of the other liquid medium and the liquid medium of the second liquid medium at the end are compatible with each other, and at 1 atm and 25 ° C. It is more preferable that they are compatible with each other.
  • the first liquid medium and the second liquid medium may be compatible with each other under the conditions of 1 atm and 25 ° C., or may not be compatible with each other under the same conditions.
  • the mixture was replaced with another liquid medium having a viscosity lower than that of the first liquid medium (however, excluding the first liquid medium and the second liquid medium) to reduce impurities in the dispersion. Later, it can be finally replaced with a second liquid medium having a higher viscosity than other liquid media (excluding the first liquid medium and the second liquid medium).
  • the viscosity of the liquid medium can be measured by, for example, a vibration viscometer or a rotary viscometer.
  • each step of replacement with the second liquid medium is preferably carried out in the absence of the organic polymer, and more preferably carried out in the absence of the organic polymer throughout the entire steps of the production method of the present invention.
  • the organic polymer and the raw material containing the organic polymer are used. It's okay if it doesn't exist.
  • the sintering of the copper particles is sufficiently advanced when the bonding composition is sintered while maintaining a low degree of aggregation of the copper particles. Can be made to.
  • the content of residual organic matter which is one of the impurities and can be a sintering inhibitor component, can be reduced, so that the density is high and the adhesion to other members is further excellent.
  • Examples of the above-mentioned organic polymer include natural polymers and synthetic polymers used as dispersants and surface treatment agents in the technical field. Details include, for example, proteins such as gelatin, and natural polymers such as gum arabic, casein, sodium caseinate, ammonium caseinate, starch, dextrin, agar, and sodium alginate. Synthetic polymers include cellulose compounds such as hydroxyethyl cellulose, carboxymethyl cellulose, methyl cellulose and ethyl cellulose, polyvinyl compounds such as polyvinyl alcohol, and polyacrylic acid compounds such as sodium polyacrylate and ammonium polyacrylate. Can be mentioned.
  • the bonding composition obtained through the above steps is a dispersion containing copper particles and a second liquid medium.
  • the bonding composition may contain only the second liquid medium as the liquid medium constituting the composition, or in addition to the second liquid medium, the liquid medium used for the liquid medium replacement up to that point. May be inevitably included. In any case, it is preferable that the second liquid medium is contained in the largest amount as a mass ratio among all the liquid media constituting the bonding composition.
  • the bonding composition is conductive as it is or, if necessary, by further adding at least one of metal particles other than copper particles contained in the bonding composition, a liquid medium, a binder resin, and the like. It can be used in the form of paste or conductive ink. That is, the present invention contains at least a bonding composition obtained through the above steps, and the composition and, if necessary, metal particles other than copper particles, a liquid medium, and a binder contained in the bonding composition. It also includes a method for producing a conductive paste in which at least one of the resins is further mixed.
  • Examples of the metal particles that can be further added to the bonding composition include particles containing metals such as copper, silver and gold.
  • the liquid medium that can be further added to the bonding composition is, for example, the same as that exemplified in the above description of the first liquid medium and the second liquid medium, and has good compatibility with the binder resin. Can be used.
  • Examples of the binder resin that can be further added to the bonding composition include one or more of acrylic resin, epoxy resin, polyester resin, polycarbonate resin, cellulose resin, and the like.
  • the bonding composition can be arranged between any two materials to be joined by a predetermined means or the like, and the two materials to be joined can be joined to form a joining structure. That is, the present invention also includes a method of arranging a bonding composition between two materials to be joined to join the materials to be joined and a method of manufacturing a bonding structure.
  • a substrate, a semiconductor element, or the like can be used independently of each other. As a specific embodiment, for example, it can be used as a bonding agent for surface mounting an electronic device on a printed wiring board or as a material for filling vias in a printed wiring board. Further, it can be used for forming a wiring circuit of a printed wiring board or forming an electrode of a chip component.
  • the present invention has been described above based on the preferred embodiment, the present invention is not limited to the above embodiment.
  • the obtained copper particles inevitably contain a trace amount of other elements, and the surface of the copper particles is inevitably a trace amount. It does not exclude being oxidized.
  • Example 1 In this example, a bonding composition was produced in the absence of an organic polymer in each step.
  • (1) Generation of Copper Particles by Wet Reduction Method In a 36 liter stainless steel tank, a mixed liquid medium of 5.0 liters of warm pure water and 5.0 liters of methanol as the first liquid medium and 2.5 kg of acetic acid as the copper source. Copper was added and stirred at a liquid temperature of 40 ° C. for 30 minutes to dissolve copper acetate. Next, 150 g of hydrazine was added all at once to the liquid medium, and then stirring was continued at a liquid temperature of 40 ° C. for 30 minutes to generate copper oxide particles in the liquid medium.
  • the first liquid medium was replaced with another liquid medium a plurality of times, and then the second liquid medium was replaced as the final replacement. All steps were carried out while maintaining the wet state of the dispersion.
  • the first other liquid medium pure water compatible with the first liquid medium was used.
  • the first liquid medium dispersion of copper particles was washed with pure water until the conductivity became 3.5 mS by a decantation method to obtain a first dispersion in which copper particles were dispersed in water.
  • the first dispersion remained moist.
  • a modified alcohol a mixed liquid medium of 89% by mass of ethanol and 11% by mass of 2-propanol
  • the first dispersion was washed with a modified alcohol with a rotary filter until the water concentration in the first dispersion became 1% by mass or less to obtain a second dispersion in which copper particles were dispersed in the modified alcohol.
  • This second dispersion remained moist.
  • hexylene glycol compatible with the second other liquid medium was used as the second liquid medium used for the final substitution.
  • hexylene glycol is solid-liquid separated by pressure filtration, and copper particles are used as the second liquid medium.
  • a bonding composition dispersed in the above was obtained. This bonding composition maintained a wet state with a solid content concentration of 92%.
  • bonding paste 7.6 parts by mass of the bonding composition, 3 parts by mass of metal particles (copper particles, 1200YF, manufactured by Mitsui Metal Mining Co., Ltd.) other than copper particles contained in the bonding composition.
  • metal particles copper particles, 1200YF, manufactured by Mitsui Metal Mining Co., Ltd.
  • 0.5 parts by mass of BIS-TRIS / hexylene glycol solution having a solid content concentration of 50% by mass and 0.1 parts by mass of polyethylene glycol 300 were mixed, and hexylene glycol was used as the balance to adjust the concentration of copper particles.
  • a bonding paste containing copper particles was prepared so as to have a mass content of 76% by mass.
  • Example 1 Similar to Example 1, (1) after the copper particles were generated by the wet reduction method, the first liquid medium dispersion of the copper particles was washed with pure water by the decantation method until the conductivity became 3 mS. , Obtained a dispersion in which copper particles were dispersed in water. This dispersion remained moist. Next, the dispersion was heated to 50 ° C., and while stirring, a dimethylglyoxime / methanol solution was added so that the dimethylglyoxime content was 0.5% by mass with respect to the copper particle content, and the liquid temperature was 50. The mixture was stirred at ° C. for 1 hour to obtain a water / methanol dispersion of surface-treated copper particles. Then, the surface-treated copper particles were vacuum-dried to obtain dried copper particles. There is no liquid medium in these copper particles. Finally, instead of the bonding composition, dried copper particles were used to prepare a bonding paste having the same composition and concentration as in Example 1.
  • the bonding pastes of Examples and Comparative Examples are screen-printed on the center surface of a copper plate (length 20 mm x width 20 mm x thickness 2 mm) with dimensions of 10 mm in length ⁇ 10 mm in width ⁇ 110 ⁇ m in thickness, and the paste for bonding is printed at 110 ° C. It was dried for 20 minutes to obtain a dry film.
  • an alumina plate (length 5 mm ⁇ width 5 mm ⁇ thickness 0.5 mm) whose surface is Ag-plated is placed on a dry film and baked at 6 MPa in a nitrogen atmosphere at a heating rate of 120 ° C./min at 280 ° C. for 20 minutes. The copper plate and the alumina plate were joined together.
  • the region where the alumina plate is arranged is indicated by reference numeral A
  • the region where the sintered body of the dried film exists is indicated by reference numeral B
  • the region where the copper plate is exposed is indicated by reference numeral C.
  • FIG. 1A in the sintered body of the paste obtained by using the bonding composition of Example 1, the region A in which the alumina plate is arranged is observed to be dark in color. It can be seen that a dense structure with few voids is formed and the bonding state between the alumina plate and the copper plate is good. Further, in the region B where the sintered body is located on the outer periphery of the alumina plate, the observed color was uniform, and peeling between the sintered body and the copper plate was not observed. Therefore, it can be seen that the paste using the bonding composition of Example 1 is excellent in adhesion to other members.
  • the region A in which the alumina plate is arranged is observed to be dark in color. Therefore, it can be seen that the bonding state between the alumina plate and the copper plate is good, but in the region B where the sintered body is located on the outer periphery of the alumina plate, the observed color is non-uniform, and the sintered body and the sintered body are in a non-uniform state. Many peelings from the copper plate were observed. Therefore, it can be seen that the paste using the bonding composition of Comparative Example 1 is inferior in adhesion to other members.

Abstract

The present invention is a method for producing a bonding composition comprising copper particles and a second solvent. In the production method, a dispersion of copper particles is prepared by producing the copper particles in a first solvent by a wet reduction method. Then, while maintaining a wet state for the dispersion, the first solvent in the dispersion is replaced ultimately with a second solvent. Replacing the first solvent with another solvent at least once and using the second solvent for the final replacement is also preferred. Carrying out solvent replacement at below 100°C is also preferred. The use as the second solvent of at least one selected from water, alcohols, ketones, esters, ethers, and hydrocarbons is also preferred.

Description

接合用組成物の製造方法Method for producing bonding composition
 本発明は、接合用組成物の製造方法に関する。 The present invention relates to a method for producing a bonding composition.
 電子機器の小型化や高性能化に伴って、電子機器内の電子回路形成において、寸法安定性や導電性、部材との密着性等の各種性能の向上が求められている。これらの要求を実現するために、例えば粒子どうしの凝集が少ない金属粉を含む導電性ペーストが望まれている。 With the miniaturization and higher performance of electronic devices, various performance improvements such as dimensional stability, conductivity, and adhesion to members are required in the formation of electronic circuits in electronic devices. In order to realize these requirements, for example, a conductive paste containing a metal powder having less agglutination between particles is desired.
 特許文献1には、湿式還元法により金属粉末を析出させる工程と、水分が付着した状態の金属粉末に水溶性有機溶剤を添加して、水分を水溶性有機溶剤で置換する工程とを備える、導電性ペーストの製造方法が開示されている。
 特許文献2には、金属粉末に対して水又は有機溶剤による洗浄を解砕とともに行う導電性ペースト用金属粉末の製造方法が開示されている。
 上述の各特許文献にはそれぞれ、金属粉末の分散性を向上できることも開示されている。
Patent Document 1 includes a step of precipitating a metal powder by a wet reduction method and a step of adding a water-soluble organic solvent to the metal powder in a state where water is attached and replacing the water with the water-soluble organic solvent. A method for producing a conductive paste is disclosed.
Patent Document 2 discloses a method for producing a metal powder for a conductive paste, in which the metal powder is washed with water or an organic solvent together with crushing.
It is also disclosed in each of the above-mentioned patent documents that the dispersibility of the metal powder can be improved.
 また、特許文献3には、銀含有粒子と界面活性剤との分散液を真空凍結乾燥させる銀含有粉末の製造方法が開示されている。
 更に特許文献4には、湿式還元法により得られた銀粒子を所定の含水率を有するウェットケーキとし、該ウェットケーキに分散剤を添加して砕解して得られた銀粉が開示されている。
 これらの特許文献には、特許文献1及び2と同様に、金属粉末の分散性を向上できることも開示されている。
Further, Patent Document 3 discloses a method for producing a silver-containing powder in which a dispersion liquid of silver-containing particles and a surfactant is vacuum freeze-dried.
Further, Patent Document 4 discloses a silver powder obtained by converting silver particles obtained by a wet reduction method into a wet cake having a predetermined water content and crushing the wet cake by adding a dispersant. ..
Similar to Patent Documents 1 and 2, these patent documents also disclose that the dispersibility of the metal powder can be improved.
特開2003-151381号公報Japanese Unexamined Patent Publication No. 2003-151381 特開2003-253301号公報Japanese Unexamined Patent Publication No. 2003-253301 US2009/146117A1US2009 / 146117A1 特開2007-224422号公報Japanese Unexamined Patent Publication No. 2007-224422
 特許文献1~4に記載の技術はいずれも、金属粒子の分散性について検討されているが、得られた金属粉又は該金属粉を含む導電性ペーストを用いて焼結に供したときの、他の部材との密着性に関しては何ら検討されていない。 All of the techniques described in Patent Documents 1 to 4 have investigated the dispersibility of metal particles, but when the obtained metal powder or a conductive paste containing the metal powder is used for sintering, No studies have been made on the adhesion to other members.
 本発明は、焼結時において、他の部材との密着性に優れる接合用組成物の製造方法を提供することにある。 The present invention is to provide a method for producing a bonding composition having excellent adhesion to other members at the time of sintering.
 本発明は、湿式還元法によって第1液媒中に銅粒子を生成させて、該銅粒子の分散体を調製し、然る後に、
 前記分散体の湿潤状態を維持しながら、該分散体の第1液媒を最終的に第2液媒に置換して、前記銅粒子と第2液媒とを含む接合用組成物を得る、接合用組成物の製造方法を提供するものである。
In the present invention, copper particles are generated in the first liquid medium by a wet reduction method to prepare a dispersion of the copper particles, and then, after that,
While maintaining the wet state of the dispersion, the first liquid medium of the dispersion is finally replaced with the second liquid medium to obtain a bonding composition containing the copper particles and the second liquid medium. It provides a method for producing a bonding composition.
図1(a)及び(b)は、実施例及び比較例の接合用組成物を接合対象物とともに焼成して得られた焼結体の超音波画像である。1 (a) and 1 (b) are ultrasonic images of a sintered body obtained by firing the bonding compositions of Examples and Comparative Examples together with an object to be bonded.
 以下本発明を、その好ましい実施形態に基づき説明する。本発明の方法は、銅粒子と、第2液媒とを含む接合用組成物の製造に関するものである。接合用組成物は、例えば、2つの接合対象物どうしを接合したりするための導電性ペーストや導電性インクとして好適に用いられる。この場合、接合用組成物は、好ましくは導電性フィラーとしての銅粒子と、第2液媒とを含む分散体である。 Hereinafter, the present invention will be described based on its preferred embodiment. The method of the present invention relates to the production of a bonding composition containing copper particles and a second liquid medium. The bonding composition is suitably used, for example, as a conductive paste or a conductive ink for bonding two objects to be bonded to each other. In this case, the bonding composition is preferably a dispersion containing copper particles as a conductive filler and a second liquid medium.
 本発明の製造方法は、湿式還元法によって第1液媒中に銅粒子を生成させて、銅粒子の分散体を調製する工程と、分散体の湿潤状態を維持しながら、分散体の第1液媒を最終的に第2液媒に置換する工程との二つに大別される。
 ここでいう「湿潤状態」とは、銅粒子を例えば熱処理等によって乾燥させないものであって、銅粒子の表面が濡れており気相と銅粒子が直接接触しない状態をいう。詳細には、銅粒子の液媒分散体の固形分濃度が95質量%以下に維持された状態を指す。
The production method of the present invention includes a step of producing copper particles in the first liquid medium by a wet reduction method to prepare a dispersion of copper particles, and a first step of the dispersion while maintaining a wet state of the dispersion. It is roughly divided into two steps, the step of finally replacing the liquid medium with the second liquid medium.
The "wet state" as used herein means a state in which the copper particles are not dried by, for example, heat treatment, and the surface of the copper particles is wet so that the vapor phase and the copper particles do not come into direct contact with each other. Specifically, it refers to a state in which the solid content concentration of the liquid medium dispersion of copper particles is maintained at 95% by mass or less.
 また、「第1液媒を最終的に第2液媒に置換する」とは、第1液媒を直接第2液媒に置換して、最終目的物である第2液媒を含む分散体を得る場合、及び、第1液媒を、第2液媒以外の一種又は二種以上の他の液媒(第1液媒及び第2液媒を除く)と置換し、最終の液媒置換工程において、他の液媒(第1液媒及び第2液媒を除く)を第2液媒に置換して、最終目的物である第2液媒を含む分散体を得る場合の双方の態様を包含する。 Further, "finally replacing the first liquid medium with the second liquid medium" means that the first liquid medium is directly replaced with the second liquid medium, and the dispersion containing the second liquid medium, which is the final object, is contained. And, the first liquid medium is replaced with one or more other liquid media (excluding the first liquid medium and the second liquid medium) other than the second liquid medium, and the final liquid medium replacement In both aspects, in the step, another liquid medium (excluding the first liquid medium and the second liquid medium) is replaced with the second liquid medium to obtain a dispersion containing the second liquid medium which is the final target product. Including.
 まず、湿式還元法によって、液媒中に銅粒子を生成させる。湿式還元法は、例えば、銅源である銅化合物と、還元性化合物とを第1液媒中に混合して反応液を調製し、該反応液中の銅化合物を還元して、目的とする銅粒子を得る。銅粒子を湿式還元法によって製造することによって、粒子の粒子径の制御が容易となり、且つ球状の粒子を簡便に得ることができる。銅粒子は、例えば特開2015-168878号公報に記載の方法で製造することもできる。 First, copper particles are generated in the liquid medium by the wet reduction method. The wet reduction method is intended, for example, by mixing a copper compound as a copper source and a reducing compound in a first liquid medium to prepare a reaction solution, and reducing the copper compound in the reaction solution. Obtain copper particles. By producing the copper particles by the wet reduction method, the particle size of the particles can be easily controlled, and spherical particles can be easily obtained. Copper particles can also be produced, for example, by the method described in Japanese Patent Application Laid-Open No. 2015-168878.
 銅化合物と還元性化合物とを含む反応液の調製にあたり、銅化合物及び還元性化合物の添加順序や方法に特に制限はない。例えば、固形の銅化合物と、固形の還元性化合物とを同時に添加して反応液としてもよい。また、銅化合物及び還元性化合物の少なくとも一方を予め液媒中に分散又は溶解させた後、一方を他方に添加して、反応液を調製してもよい。銅化合物及び還元性化合物のうち一方を他方に添加する場合、一度に添加してもよく、例えば滴下等の方法で、連続的又は断続的に添加してもよい。 In preparing the reaction solution containing the copper compound and the reducing compound, there are no particular restrictions on the order and method of adding the copper compound and the reducing compound. For example, a solid copper compound and a solid reducing compound may be added at the same time to prepare a reaction solution. Further, at least one of the copper compound and the reducing compound may be dispersed or dissolved in the liquid medium in advance, and then one may be added to the other to prepare a reaction solution. When one of the copper compound and the reducing compound is added to the other, it may be added all at once, or may be added continuously or intermittently by a method such as dropping.
 銅化合物としては、液媒に溶解する化合物を用いることが好ましい。このような銅化合物としては、例えば塩化銅、酢酸銅、硫酸銅等の水溶性銅(II)塩等が挙げられる。これらの銅化合物は、無水物であってもよく、水和物であってもよい。これらの銅化合物は、単独で又は複数組み合わせて用いることができる。 As the copper compound, it is preferable to use a compound that dissolves in a liquid medium. Examples of such a copper compound include water-soluble copper (II) salts such as copper chloride, copper acetate and copper sulfate. These copper compounds may be anhydrous or hydrated. These copper compounds can be used alone or in combination of two or more.
 銅化合物は、反応液中の銅元素の含有量に換算して、好ましくは0.001mol/L以上1mol/L以下、更に好ましくは0.1mol/L以上0.5mol/L以下となるように混合する。このような銅化合物の含有量とすることによって、粒子径が小さい銅粒子を生産性高く得ることができる。 The copper compound is preferably 0.001 mol / L or more and 1 mol / L or less, and more preferably 0.1 mol / L or more and 0.5 mol / L or less in terms of the content of the copper element in the reaction solution. Mix. By setting the content of such a copper compound, copper particles having a small particle size can be obtained with high productivity.
 還元性化合物は、銅源の銅イオンを還元するものである。還元性化合物としては、例えば、ヒドラジン、塩酸ヒドラジン、硫酸ヒドラジン及び抱水ヒドラジン等のヒドラジン系化合物、水素化ホウ素ナトリウム、亜硫酸ナトリウム、亜硫酸水素ナトリウム、チオ硫酸ナトリウム、亜硝酸ナトリウム、次亜硝酸ナトリウム、亜リン酸、亜リン酸ナトリウム、次亜リン酸、及び次亜リン酸ナトリウム等が挙げられる。これらの還元性化合物は、無水物であってもよく、水和物であってもよい。これらの還元性化合物は一種を単独で、又は二種以上を組み合わせて用いることができる。
 特に、ヒドラジンは還元後に不純物の発生や、得られる銅粒子への不純物の混入が少ないので特に好適に用いられる。還元力が強く、且つ粒子への不純物の混入を抑制する観点から、還元性化合物として、ヒドラジンの無水物又は水和物のみを用いることがより一層好ましい。
The reducing compound reduces the copper ions of the copper source. Examples of the reducing compound include hydrazine compounds such as hydrazine, hydrazine hydrochloride, hydrazine sulfate and hydrous hydrazine, sodium hydride, sodium sulfite, sodium hydrogen sulfite, sodium thiosulfate, sodium nitrite, sodium hyponitrite, and the like. Examples thereof include phosphite, sodium phosphite, hypophosphite, and sodium hypophosphite. These reducing compounds may be anhydrous or hydrated. These reducing compounds may be used alone or in combination of two or more.
In particular, hydrazine is particularly preferably used because it causes less impurities to be generated after reduction and less impurities are mixed into the obtained copper particles. From the viewpoint of strong reducing power and suppressing contamination of particles with impurities, it is more preferable to use only hydrazine anhydride or hydrate as the reducing compound.
 反応液中の還元性化合物の含有量は、銅元素1molに対して、好ましくは0.5mol以上50mol以下、より好ましくは1mol以上10mol以下、更に好ましくは2mol以上5mol以下となるように混合する。還元性化合物の含有量をこのような割合とすることによって、粒子径が小さい銅粒子を容易に得ることができる。還元性化合物による銅化合物の還元は、一回のみ行ってもよく、必要に応じて複数回行ってもよい。上述した還元性化合物の含有量は、無水物換算での値とする。 The content of the reducing compound in the reaction solution is preferably 0.5 mol or more and 50 mol or less, more preferably 1 mol or more and 10 mol or less, and further preferably 2 mol or more and 5 mol or less with respect to 1 mol of the copper element. By setting the content of the reducing compound to such a ratio, copper particles having a small particle size can be easily obtained. The reduction of the copper compound by the reducing compound may be carried out only once, or may be carried out a plurality of times as necessary. The content of the reducing compound described above is a value in terms of anhydride.
 反応液の反応条件は、混合開始時点から反応終了時点にわたって、加熱せずに反応させてもよく、加熱条件下で反応させてもよい。
 また、還元反応を均一に発生させて、粒径のばらつきが少ない銅粒子を得る観点から、混合開始時点から反応終了時点までの全時間において、反応液の撹拌を継続することも好ましい。
The reaction conditions of the reaction solution may be the reaction without heating from the start of mixing to the end of the reaction, or the reaction may be carried out under heating conditions.
Further, from the viewpoint of uniformly generating the reduction reaction and obtaining copper particles having little variation in particle size, it is also preferable to continue stirring the reaction solution for the entire time from the start of mixing to the end of the reaction.
 銅粒子の形成に十分な還元反応の進行と、製造コストの低減とを両立させる観点から、混合開始時点から反応終了時点にわたって、0℃以上80℃以下を維持するように反応させることが好ましい。混合開始時点から反応終了時点までの時間は、目的とする銅粒子の粒子径によって適宜変更可能であるが、好ましくは0.5時間以上4時間以下、更に好ましくは1時間以上3時間以下とすることができる。還元性化合物による銅化合物の還元処理を複数回行う場合、上述の時間は、各回の混合開始時点から反応終了時点までの時間の合計とする。 From the viewpoint of achieving both the progress of the reduction reaction sufficient for the formation of copper particles and the reduction of the production cost, it is preferable to carry out the reaction so as to maintain 0 ° C. or higher and 80 ° C. or lower from the start time of mixing to the end time of the reaction. The time from the start of mixing to the end of the reaction can be appropriately changed depending on the particle size of the target copper particles, but is preferably 0.5 hours or more and 4 hours or less, and more preferably 1 hour or more and 3 hours or less. be able to. When the reduction treatment of the copper compound with the reducing compound is performed a plurality of times, the above-mentioned time is the total of the time from the start time of each mixing to the end time of the reaction.
 以上の工程を経て、銅粒子を生成させる。銅粒子は、湿式還元法によって得られたものであるので、反応液の液媒である第1液媒に分散した銅粒子の分散体の状態となっている。 Copper particles are generated through the above steps. Since the copper particles are obtained by the wet reduction method, they are in the state of a dispersion of copper particles dispersed in the first liquid medium which is the liquid medium of the reaction liquid.
 生成した銅粒子は、その粒子径が、走査型電子顕微鏡観察の画像解析によって測定された累積体積50容量%における体積累積粒径DSEM50で表して、好ましくは100nm以上300nm以下、より好ましくは100nm以上250nm以下である。DSEM50は、外形上の幾何学的形態から判断して、粒子としての最小単位と認められる物体である一次粒子の粒子径を示しているので、銅粒子をこのような粒子径の範囲とすることによって、接合用組成物は良好な充填性且つ焼結性を発現し、接合対象物等の他の部材との高い密着性を発現可能であり且つ薄い塗膜を形成することに有利である。銅粒子の粒子径は、例えば、銅化合物と還元性化合物とのモル比を調整したり、還元反応の時間を調整したりすることによって、適宜調整することができる。 The generated copper particles are preferably 100 nm or more and 300 nm or less, more preferably 100 nm, represented by the volume cumulative particle size DSEM50 at a cumulative volume of 50% by volume measured by image analysis of scanning electron microscope observation. It is 250 nm or more and 250 nm or less. Since D SEM50 indicates the particle size of the primary particle, which is an object recognized as the smallest unit as a particle, judging from the geometrical shape on the outer shape, the copper particle is defined as such a particle size range. As a result, the bonding composition exhibits good packing properties and sinterability, is capable of exhibiting high adhesion to other members such as the object to be bonded, and is advantageous in forming a thin coating film. .. The particle size of the copper particles can be appropriately adjusted, for example, by adjusting the molar ratio of the copper compound and the reducing compound, or by adjusting the time of the reduction reaction.
 DSEM50は、例えば以下の方法で測定することができる。まず、マウンテック社製ソフトウェアのMac-Viewを用い、走査型電子顕微鏡により真上から観察して得られた銅粒子の画像データを読み込んだ後、データ上の銅粒子を無作為に50個以上選んで、該粒子の粒径(ヘイウッド径)を測定する。次いで、得られたヘイウッド径から、粒子が真球であると仮定したときの体積を算出し、該体積の累積体積50容量%における体積累積粒径をDSEM50とする。 D SEM50 can be measured by, for example, the following method. First, using Mac-View, a software manufactured by Mountech, the image data of copper particles obtained by observing from directly above with a scanning electron microscope was read, and then 50 or more copper particles on the data were randomly selected. Then, the particle size (Haywood diameter) of the particles is measured. Next, from the obtained Haywood diameter, the volume when the particles are assumed to be true spheres is calculated, and the volume cumulative particle diameter at 50% by volume of the cumulative volume of the volume is defined as DSEM50 .
 続いて、銅粒子分散体の湿潤状態を維持しながら、該分散体の第1液媒を第2液媒に置換する。本工程では、目的とする接合用組成物を得るにあたり、分散体の湿潤状態を維持しながら、該分散体中の第1液媒を、接合用組成物に最終的に含まれる液媒である第2液媒に置換することを特徴の一つとしている。 Subsequently, the first liquid medium of the dispersion is replaced with the second liquid medium while maintaining the wet state of the copper particle dispersion. In this step, in obtaining the desired bonding composition, the first liquid medium in the dispersion is finally contained in the bonding composition while maintaining the wet state of the dispersion. One of the features is to replace it with a second liquid medium.
 導電性フィラーとして銅粒子を含む導電性ペーストや導電性インク等の接合用組成物の調製においては、典型的には、得られた銅粒子を乾燥させた乾燥銅粉を用いる。この方法では、銅粒子の含有量を適宜増減させて、所望のフィラー濃度を有するペーストやインクを容易に調製可能である。しかし、乾燥銅粉を用いて接合用組成物を調製する場合、乾燥銅粉中の銅粒子どうしが凝集したり、又は凝集しやすくなっていることに起因して、再分散の処理が煩雑となったり、再分散自体が不可能になったりすることがあった。その結果、接合用組成物の塗布によって得られた塗膜は平滑になりづらく、他の部材との密着性に劣るものとなっていた。また、乾燥時に銅粒子の表面が酸化等により変質して、密着性や導電性等の所望の特性を発現できないことがあった。
 特に、インクやペーストに好適な粒径を有する銅粒子を乾燥状態で用いる場合、再分散の煩雑さや、酸化等による粒子の変質が顕著となっていた。
In the preparation of a bonding composition such as a conductive paste containing copper particles or a conductive ink as a conductive filler, dried copper powder obtained by drying the obtained copper particles is typically used. In this method, the content of copper particles can be appropriately increased or decreased to easily prepare a paste or ink having a desired filler concentration. However, when a bonding composition is prepared using dried copper powder, the redispersion process becomes complicated because the copper particles in the dried copper powder are agglomerated or easily agglomerated. In some cases, redispersion itself became impossible. As a result, the coating film obtained by applying the bonding composition is difficult to be smooth and has poor adhesion to other members. In addition, the surface of the copper particles may be altered by oxidation or the like during drying, and desired properties such as adhesion and conductivity may not be exhibited.
In particular, when copper particles having a particle size suitable for ink or paste are used in a dry state, the complexity of redispersion and the deterioration of the particles due to oxidation and the like are remarkable.
 この問題点を解決すべく本発明者が検討したところ、得られた銅粒子を乾燥させずに、湿潤状態を維持したまま以後の工程に供することによって、銅粒子と大気中の酸素の接触が低減される。更に接合用組成物を調製する際の銅粒子の分散性が高くなることで、成膜及び焼結時における過剰な応力発生が抑制される。その結果、本発明の接合用組成物は、焼結時に他の部材との優れた密着性を発現するとともに、焼結時において過剰な体積収縮に起因する他部材からの剥離を抑制できることを見出した。 As a result of investigation by the present inventor in order to solve this problem, the copper particles obtained are not dried and are subjected to the subsequent steps while being maintained in a wet state, so that the copper particles come into contact with oxygen in the atmosphere. It will be reduced. Further, by increasing the dispersibility of the copper particles when preparing the bonding composition, excessive stress generation during film formation and sintering is suppressed. As a result, it has been found that the bonding composition of the present invention can exhibit excellent adhesion to other members during sintering and can suppress peeling from other members due to excessive volume shrinkage during sintering. rice field.
 第1液媒から第2液媒への置換は直接行ってもよく(以下、これを「直接置換」ともいう。)、第1液媒から他の液媒(ただし、第2液媒は除く。)に一回以上置換した後で、第2液媒に最終的に置換してもよい(以下、これを「間接置換」ともいう。)。湿潤状態を維持した分散体は、それぞれ独立して、例えば、スラリーや、ウェットケーキの態様であり得る。 Substitution of the first liquid medium to the second liquid medium may be performed directly (hereinafter, this is also referred to as "direct replacement"), and the first liquid medium to another liquid medium (however, the second liquid medium is excluded). ) May be replaced one or more times, and then finally replaced with a second liquid medium (hereinafter, this is also referred to as "indirect replacement"). The dispersions maintained in a wet state can be independently, for example, in the form of a slurry or a wet cake.
 液媒の置換方法は、直接置換及び間接置換を問わず、分散体の湿潤状態を維持可能であれば特に制限はなく、例えば、リパルプ洗浄やデカンテーション法、ロータリーフィルター法、ろ過等を採用することができる。また、液媒の置換は、1回のみ行ってもよく、必要に応じて複数回行ってもよい。 The method for replacing the liquid medium is not particularly limited as long as the wet state of the dispersion can be maintained regardless of direct substitution or indirect substitution. For example, repulp washing, decantation method, rotary filter method, filtration and the like are adopted. be able to. Further, the liquid medium may be replaced only once, or may be performed a plurality of times as needed.
 直接置換及び間接置換を問わず、液媒の置換は、液媒の温度を好ましくは100℃未満、より好ましくは80℃以下、更に好ましくは60℃以下に設定して行う。このような温度に設定して行うことによって、置換時における液媒の蒸発を抑制し、湿潤状態と、銅粒子の高い分散性とを維持しながら、他の部材との密着性に優れる接合用組成物を得ることができる。 Regardless of direct substitution or indirect substitution, the liquid medium is replaced by setting the temperature of the liquid medium to preferably less than 100 ° C., more preferably 80 ° C. or lower, and further preferably 60 ° C. or lower. By setting such a temperature, evaporation of the liquid medium at the time of replacement is suppressed, and while maintaining a wet state and high dispersibility of copper particles, for bonding having excellent adhesion to other members. The composition can be obtained.
 第1液媒を最終的に第2液媒に置換する過程において、不純物の原因となり得る第1液媒由来の成分を効率よく除去するとともに、目的とする接合用組成物に含有する第2液媒への置換の作業性を高める観点から、湿式還元法によって得られた銅粒子分散体に含まれる第1液媒を他の液媒(ただし、第1液媒及び第2液媒を除く。)に一回以上置換し、最終の置換に第2液媒を用いることが好ましい。つまり、本製造方法として、間接置換を採用することが好ましい。 In the process of finally replacing the first liquid medium with the second liquid medium, the components derived from the first liquid medium that can cause impurities are efficiently removed, and the second liquid contained in the target bonding composition. From the viewpoint of improving the workability of replacement with a medium, the first liquid medium contained in the copper particle dispersion obtained by the wet reduction method is excluded from other liquid media (however, the first liquid medium and the second liquid medium are excluded. ) Is replaced at least once, and a second liquid medium is preferably used for the final replacement. That is, it is preferable to adopt indirect substitution as the present production method.
 また、第1液媒を他の液媒(ただし、第2液媒は除く。)に複数回置換する場合においても同様に、第1液媒から最初の他の液媒への置換、他の液媒を二種以上用いる場合の他の液媒間での置換、及び最後の他の液媒から第2液媒への置換の各工程において、分散体の湿潤状態を維持して置換を行うことが好ましい。
 第1液媒を他の液媒に一回以上置換する場合、各置換工程での固形分濃度はそれぞれ独立して、同一であってもよく、異なってもよい。
 銅粒子の湿潤状態を維持して液媒を置換することによって、不純物の原因となり得る第1液媒由来の成分を効率よく除去しつつ、再分散性が高く且つ変質が少ない銅粒子を得ることができるので、該銅粒子含む接合用組成物を焼結したときに、他の部材と密着性を一層優れたものとすることができる。
Further, when the first liquid medium is replaced with another liquid medium (however, the second liquid medium is excluded) multiple times, similarly, the first liquid medium is replaced with the first other liquid medium, and other liquid mediums are replaced. In each step of replacement between other liquid media when two or more liquid media are used, and replacement from the last other liquid medium to the second liquid medium, the dispersion is replaced while maintaining a wet state. Is preferable.
When the first liquid medium is replaced with another liquid medium more than once, the solid content concentration in each replacement step may be the same or different.
By replacing the liquid medium while maintaining the wet state of the copper particles, it is possible to obtain copper particles having high redispersibility and little deterioration while efficiently removing components derived from the first liquid medium that can cause impurities. Therefore, when the bonding composition containing the copper particles is sintered, the adhesion to other members can be further improved.
 第1液媒を他の液媒に一回以上置換する方法の一実施形態としては、例えば、湿式還元法によって得られた銅粒子の第1液媒分散体を、水等の他の液媒を用いて洗浄処理する方法が挙げられる。
 洗浄処理を行う場合、その方法としては、例えば、リパルプ洗浄やデカンテーション法、ロータリーフィルター法、ろ過等を採用することができる。洗浄処理を行う場合、洗浄後の銅粒子は湿潤状態を維持した分散体の状態で、以後の工程に供することが好ましい。
As one embodiment of the method of substituting the first liquid medium with another liquid medium one or more times, for example, the first liquid medium dispersion of copper particles obtained by the wet reduction method is used as another liquid medium such as water. There is a method of cleaning treatment using.
When the cleaning treatment is performed, for example, repulp cleaning, decantation method, rotary filter method, filtration and the like can be adopted as the method. When the cleaning treatment is performed, it is preferable that the copper particles after cleaning are subjected to the subsequent steps in the state of a dispersion that maintains a wet state.
 デカンテーション法で銅粒子を洗浄処理する場合、例えば他の液媒を添加して、分散体の導電率を好ましくは5mS以下となるまで洗浄を行う。このときの洗浄条件は、例えば、他の液媒として水を用いた場合、洗浄温度は、好ましくは100℃未満であり、更に好ましくは15℃以上30℃以下とする。このような条件で行うことによって、銅粒子に含まれる不純物を低減しつつ、粒子どうしが均一に分散したままで、以後の工程に供することができる。その後、洗浄した銅粒子の液媒分散体を、湿潤状態を維持した状態で、第2液媒を用いて最終の置換を行う。 When the copper particles are washed by the decantation method, for example, another liquid medium is added and the dispersion is washed until the conductivity is preferably 5 mS or less. The cleaning conditions at this time are, for example, when water is used as another liquid medium, the cleaning temperature is preferably less than 100 ° C, more preferably 15 ° C or more and 30 ° C or less. By carrying out under such conditions, it is possible to reduce impurities contained in the copper particles and to use the particles in the subsequent steps while keeping the particles uniformly dispersed. Then, the liquid medium dispersion of the washed copper particles is finally replaced with the second liquid medium while maintaining the wet state.
 第1液媒を他の液媒に一回以上置換する方法の別の実施形態としては、例えば後述する実施例に記載の方法が挙げられるが、本発明の効果が奏される限りにおいて、その置換回数や、用いる液媒の種類に特に制限なく適用可能である。その後、銅粒子の液媒分散体を、湿潤状態を維持した状態で、第2液媒を用いて最終の置換を行う。 As another embodiment of the method of substituting the first liquid medium with another liquid medium one or more times, for example, the method described in Examples described later can be mentioned, but as long as the effect of the present invention is exhibited, the method is described. It can be applied without particular limitation on the number of replacements and the type of liquid medium used. Then, the liquid medium dispersion of the copper particles is finally replaced with the second liquid medium while maintaining the wet state.
 以上の工程を経て、銅粒子と第2液媒とを含む接合用組成物を得ることができる。本製造方法によれば、接合用組成物を調製する際の銅粒子の分散処理が簡便となり、また銅粒子どうしの凝集が低減されているので、平滑性の高い塗膜を効率よく形成可能となる。また、銅粒子の表面の変質を低減させることができる。その結果、接合用組成物によって形成された塗膜を焼結した際に、銅粒子どうしの溶融性を高めて、銅粒子の溶融性を高めて、溶融した粒子と他の部材との接触面積を大きくすることができる。その結果、クラックや剥離が生じにくく、他の部材との密着性に優れた焼結体を得ることができる。 Through the above steps, a bonding composition containing copper particles and a second liquid medium can be obtained. According to this production method, the dispersion treatment of copper particles when preparing a bonding composition is simplified, and the agglutination of copper particles is reduced, so that a highly smooth coating film can be efficiently formed. Become. Moreover, the deterioration of the surface of the copper particles can be reduced. As a result, when the coating film formed by the bonding composition is sintered, the meltability of the copper particles is increased, the meltability of the copper particles is increased, and the contact area between the melted particles and other members is increased. Can be increased. As a result, it is possible to obtain a sintered body that is less likely to crack or peel and has excellent adhesion to other members.
 本製造方法に用いられる第1液媒としては、湿式還元法による銅の還元を効率よく進行させる観点から、水、アルコール、ケトン、エステル及びエーテルのうち一種以上が好ましく、湿式還元法による銅粒子の製造において銅塩との相溶性を高めて銅粒子の生成効率を高める観点から、水及びアルコールのうち一種以上が更に好ましい。 As the first liquid medium used in this production method, one or more of water, alcohol, ketone, ester and ether is preferable from the viewpoint of efficiently advancing the reduction of copper by the wet reduction method, and the copper particles by the wet reduction method are used. From the viewpoint of increasing the compatibility with the copper salt and increasing the production efficiency of copper particles, one or more of water and alcohol are more preferable.
 また、本製造方法に用いられる第2液媒としては、接合用組成物をそのまま導電性ペーストや導電性インクとして使用可能にして、生産性を高める観点から、水、アルコール、ケトン、エステル、エーテル及び炭化水素のうち一種以上が好ましく、アルコール及び炭化水素を用いることが更に好ましい。
 なお、上述した第1液媒及び第2液媒は互いに同じものであってもよく、異なるものであってもよい。
Further, as the second liquid medium used in this production method, water, alcohol, ketone, ester, ether can be used as it is as a conductive paste or conductive ink from the viewpoint of increasing productivity. And one or more of hydrocarbons are preferable, and alcohol and hydrocarbons are more preferable.
The above-mentioned first liquid medium and second liquid medium may be the same as each other or may be different from each other.
 第1液媒の残存量の低減と、第2液媒への置換の容易性とを両立する観点から、他の液媒(ただし第1液媒及び第2液媒を除く)を用いる場合、他の液媒としては、水、アルコール、ケトン、エステル、エーテル及び炭化水素のうち一種以上を用いることが好ましく、水及びアルコールのうち一種以上を用いることが更に好ましい。 When using another liquid medium (excluding the first liquid medium and the second liquid medium) from the viewpoint of achieving both a reduction in the residual amount of the first liquid medium and the ease of replacement with the second liquid medium, when using another liquid medium. As the other liquid medium, it is preferable to use one or more of water, alcohol, ketone, ester, ether and hydrocarbon, and it is more preferable to use one or more of water and alcohol.
 アルコールとしては、例えば、メタノール、エタノール、n-プロパノール、2-プロパノール及びn-ブタノール等の一価アルコールや、エチレングリコール、1,2-プロピレングリコール、1,3-プロピレングリコール、ブチレングリコール、ペンチレングリコール及びヘキシレングリコール等のジオール、グリセリン等のトリオール、ポリエチレングリコールやポリプロピレングリコール等のポリオール等の多価アルコールを用いることができる。 Examples of the alcohol include monohydric alcohols such as methanol, ethanol, n-propanol, 2-propanol and n-butanol, ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, butylene glycol and pentylene. Polyhydric alcohols such as diols such as glycol and hexylene glycol, triols such as glycerin, and polyols such as polyethylene glycol and polypropylene glycol can be used.
 エステルとしては、例えば上述した多価アルコールの脂肪酸エステルが挙げられる。脂肪酸としては例えば炭素原子数が好ましくは1以上8以下、より好ましくは1以上5以下の一価脂肪酸である。多価アルコールのエステルは、少なくとも1個の水酸基を有していることが好ましい。 Examples of the ester include the fatty acid ester of the polyhydric alcohol described above. The fatty acid is, for example, a monovalent fatty acid having a carbon atom number of preferably 1 or more and 8 or less, and more preferably 1 or more and 5 or less. The ester of the polyhydric alcohol preferably has at least one hydroxyl group.
 ケトンとしては、カルボニル基に結合しているアルキル基の炭素原子数が1以上6以下、特に1以上4以下のものが好ましい。ケトンの具体例としては、メチルエチルケトン、アセトン等が挙げられる。 As the ketone, a ketone having an alkyl group bonded to a carbonyl group having 1 or more and 6 or less carbon atoms, particularly 1 or more and 4 or less is preferable. Specific examples of the ketone include methyl ethyl ketone, acetone and the like.
 エーテルとしては、ジメチルエーテル、エチルメチルエーテル、ジエチルエーテル等の鎖状エーテルや、オキタセン、テトラヒドロフラン、テトラヒドロピラン等の環状エーテルが挙げられる。 Examples of the ether include chain ethers such as dimethyl ether, ethyl methyl ether and diethyl ether, and cyclic ethers such as octacene, tetrahydrofuran and tetrahydropyran.
 炭化水素としては、ヘキサン、ヘプタン、オクタン、ノナン、デカン、ウンデカン、ドデカン、トリデカン、テトラデカン、ペンタデカン、ヘキサデカン等の脂肪族炭化水素等が挙げられる。 Examples of hydrocarbons include aliphatic hydrocarbons such as hexane, heptane, octane, nonane, decane, undecane, dodecane, tridecane, tetradecane, pentadecane, and hexadecane.
 直接置換の場合において、用いる第1液媒と第2液媒とは、1気圧、25℃の条件において互いに相溶可能であることが更に好ましい。相溶とは、二種以上の液体成分を含む流動体において、二種以上の液体成分が互いに混ざり合い、単一相を形成する現象をいう。
 相溶可能な液媒を用いることによって、第1液媒の銅粒子分散体における粒子の分散性を維持したまま第2液媒に置換することができる。これに加えて、銅粒子の変質を低減した状態で第2液媒に置換することができるので、得られる接合用組成物を焼結したときに、銅粒子の溶融性を高めて、溶融した粒子と他の部材の表面との接触面積を大きくすることができる。その結果、他の部材との密着性が高く、不純物が少ない焼結体を得ることができる。
In the case of direct substitution, it is more preferable that the first liquid medium and the second liquid medium to be used are compatible with each other under the conditions of 1 atm and 25 ° C. Compatibility means a phenomenon in which two or more kinds of liquid components are mixed with each other to form a single phase in a fluid containing two or more kinds of liquid components.
By using a compatible liquid medium, it is possible to replace the first liquid medium with the second liquid medium while maintaining the dispersibility of the particles in the copper particle dispersion. In addition to this, it can be replaced with a second liquid medium in a state where the deterioration of the copper particles is reduced, so that when the obtained bonding composition is sintered, the meltability of the copper particles is increased and the copper particles are melted. The contact area between the particles and the surface of other members can be increased. As a result, it is possible to obtain a sintered body having high adhesion to other members and few impurities.
 また間接置換の場合において、第1液媒を他の液媒に一回以上置換する場合、第1液媒及び最初の他の液媒、他の液媒を用いて二回以上置換する場合に工程上連続する他の液媒どうし、並びに最後の他の液媒及び第2液媒の各液媒の組み合わせは、いずれも互いに相溶可能であることが好ましく、1気圧、25℃の条件において互いに相溶可能であることがより好ましい。
 また、間接置換の場合、第1液媒と第2液媒とは、1気圧、25℃の条件において互いに相溶可能であってもよく、同条件で相溶不能であってもよい。
 各液媒の置換において、互いに相溶可能な液媒を用いることによって、不純物の原因となり得る第1液媒及び他の液媒由来の成分を効率よく除去することができる。その結果、他の部材との密着性が高く、不純物が少ない焼結体を得ることができる。
In the case of indirect replacement, when the first liquid medium is replaced with another liquid medium one or more times, or when the first liquid medium, the first other liquid medium, or another liquid medium is used for replacement twice or more. It is preferable that the other liquid media that are continuous in the process and the combination of the other liquid medium and the liquid medium of the second liquid medium at the end are compatible with each other, and at 1 atm and 25 ° C. It is more preferable that they are compatible with each other.
Further, in the case of indirect substitution, the first liquid medium and the second liquid medium may be compatible with each other under the conditions of 1 atm and 25 ° C., or may not be compatible with each other under the same conditions.
By using a liquid medium that is compatible with each other in the replacement of each liquid medium, it is possible to efficiently remove the components derived from the first liquid medium and other liquid media that may cause impurities. As a result, it is possible to obtain a sintered body having high adhesion to other members and few impurities.
 また、間接置換における一態様として、第1液媒よりも粘度の低い他の液媒(ただし第1液媒及び第2液媒を除く)に置換して、分散体中の不純物を減少させた後、他の液媒(ただし第1液媒及び第2液媒を除く)よりも粘度の高い第2液媒に最終的に置換することもできる。液媒の粘度は、例えば振動式粘度計や回転式粘度計により測定することができる。 Further, as one aspect of indirect substitution, the mixture was replaced with another liquid medium having a viscosity lower than that of the first liquid medium (however, excluding the first liquid medium and the second liquid medium) to reduce impurities in the dispersion. Later, it can be finally replaced with a second liquid medium having a higher viscosity than other liquid media (excluding the first liquid medium and the second liquid medium). The viscosity of the liquid medium can be measured by, for example, a vibration viscometer or a rotary viscometer.
 上述した湿式還元法による銅粒子の生成、及び第1液媒から第2液媒への置換、並びに必要に応じて、第1液媒から他の液媒への置換、及び他の液媒から第2液媒への置換の各工程において、有機高分子の非存在下で行うことが好ましく、本発明の製造方法の全工程にわたって有機高分子の非存在下で行うことが更に好ましい。
 本製造方法において、反応系中に有機高分子を非存在とするためには、例えば、還元湿式法及び液媒の置換の各工程において、有機高分子、及び有機高分子を含有する原材料を用いなければよい。
 有機高分子の非存在下で各工程を行うことによって、銅粒子の凝集の程度が低い状態を維持しつつ、接合用組成物を焼結したときに、銅粒子どうしの焼結を十分に進行させることができる。これに加えて、不純物の一つであり焼結阻害成分となり得る残存有機物の含有量を低減することができるので、高密度で且つ他の部材との密着性に一層優れたものとなる。
Generation of copper particles by the wet reduction method described above, replacement of the first liquid medium with the second liquid medium, and, if necessary, replacement of the first liquid medium with another liquid medium, and from the other liquid medium. Each step of replacement with the second liquid medium is preferably carried out in the absence of the organic polymer, and more preferably carried out in the absence of the organic polymer throughout the entire steps of the production method of the present invention.
In this production method, in order to eliminate the organic polymer in the reaction system, for example, in each step of the reduction wet method and the replacement of the liquid medium, the organic polymer and the raw material containing the organic polymer are used. It's okay if it doesn't exist.
By performing each step in the absence of the organic polymer, the sintering of the copper particles is sufficiently advanced when the bonding composition is sintered while maintaining a low degree of aggregation of the copper particles. Can be made to. In addition to this, the content of residual organic matter, which is one of the impurities and can be a sintering inhibitor component, can be reduced, so that the density is high and the adhesion to other members is further excellent.
 上述した有機高分子としては、当該技術分野において分散剤や表面処理剤として用いられる天然高分子及び合成高分子が挙げられる。詳細には、例えば、ゼラチン等のタンパク質、アラビアゴム、カゼイン、カゼイン酸ソーダ、カゼイン酸アンモニウム、デンプン、デキストリン、寒天、アルギン酸ソーダなどの天然高分子が挙げられる。合成高分子としては、ヒドロキシエチルセルロース、カルボキシメチルセルロース、メチルセルロース及びエチルセルロース等のセルロース系化合物、ポリビニルアルコール等のポリビニル系化合物、ポリアクリル酸ソーダ及びポリアクリル酸アンモニウム等のポリアクリル酸系化合物などの合成高分子が挙げられる。 Examples of the above-mentioned organic polymer include natural polymers and synthetic polymers used as dispersants and surface treatment agents in the technical field. Details include, for example, proteins such as gelatin, and natural polymers such as gum arabic, casein, sodium caseinate, ammonium caseinate, starch, dextrin, agar, and sodium alginate. Synthetic polymers include cellulose compounds such as hydroxyethyl cellulose, carboxymethyl cellulose, methyl cellulose and ethyl cellulose, polyvinyl compounds such as polyvinyl alcohol, and polyacrylic acid compounds such as sodium polyacrylate and ammonium polyacrylate. Can be mentioned.
 以上の工程を経て得られる接合用組成物は、銅粒子と第2液媒とを含む分散体である。接合用組成物は、該組成物を構成する液媒として第2液媒のみが含まれていてもよく、あるいは、第2液媒に加えて、それまでの液媒置換に用いられた液媒が不可避的に含まれていてもよい。いずれの場合であっても、接合用組成物を構成する全液媒のうち、質量割合として、第2液媒が最も多く含まれていることが好ましい。 The bonding composition obtained through the above steps is a dispersion containing copper particles and a second liquid medium. The bonding composition may contain only the second liquid medium as the liquid medium constituting the composition, or in addition to the second liquid medium, the liquid medium used for the liquid medium replacement up to that point. May be inevitably included. In any case, it is preferable that the second liquid medium is contained in the largest amount as a mass ratio among all the liquid media constituting the bonding composition.
 接合用組成物は、これをそのままで、あるいは必要に応じて、接合用組成物に含まれる銅粒子以外の金属粒子や、液媒、バインダ樹脂等のうち少なくとも一種を更に添加して、導電性ペーストや導電性インクなどの態様で用いることができる。すなわち、本発明は、上述の工程を経て得られた接合用組成物を少なくとも含み、該組成物と、必要に応じて、接合用組成物に含まれる銅粒子以外の金属粒子、液媒及びバインダ樹脂のうち少なくとも一種とを更に混合する、導電性ペーストの製造方法も包含する。 The bonding composition is conductive as it is or, if necessary, by further adding at least one of metal particles other than copper particles contained in the bonding composition, a liquid medium, a binder resin, and the like. It can be used in the form of paste or conductive ink. That is, the present invention contains at least a bonding composition obtained through the above steps, and the composition and, if necessary, metal particles other than copper particles, a liquid medium, and a binder contained in the bonding composition. It also includes a method for producing a conductive paste in which at least one of the resins is further mixed.
 接合用組成物に更に添加され得る金属粒子としては、例えば、銅、銀及び金等の金属を含む粒子が挙げられる。
 接合用組成物に更に添加され得る液媒としては、例えば上述の第1液媒や第2液媒の説明において例示したものと同様のものであり、且つバインダ樹脂との相溶性が良好であるものを用いることができる。
 接合用組成物に更に添加され得るバインダ樹脂としては、例えば、アクリル樹脂、エポキシ樹脂、ポリエステル樹脂、ポリカーボネート樹脂及びセルロース樹脂等のうち一種以上が挙げられる。
Examples of the metal particles that can be further added to the bonding composition include particles containing metals such as copper, silver and gold.
The liquid medium that can be further added to the bonding composition is, for example, the same as that exemplified in the above description of the first liquid medium and the second liquid medium, and has good compatibility with the binder resin. Can be used.
Examples of the binder resin that can be further added to the bonding composition include one or more of acrylic resin, epoxy resin, polyester resin, polycarbonate resin, cellulose resin, and the like.
 接合用組成物は、任意の2つの被接合材の間に所定の手段によって塗布する等の方法で配し、2つの被接合材どうしを接合して、接合構造とすることができる。すなわち、本発明は、2つの被接合材の間に接合用組成物を配して、被接合材を接合する方法並びに接合構造の製造方法も包含する。被接合材としては、それぞれ独立して、基板や半導体素子などを用いることができる。具体的な実施形態として例えば、プリント配線基板に電子デバイスを表面実装するときの接合剤や、プリント配線基板中のビア充填用材料として用いることができる。更に、プリント配線基板の配線回路を形成したり、チップ部品の電極形成に用いたりすることもできる。 The bonding composition can be arranged between any two materials to be joined by a predetermined means or the like, and the two materials to be joined can be joined to form a joining structure. That is, the present invention also includes a method of arranging a bonding composition between two materials to be joined to join the materials to be joined and a method of manufacturing a bonding structure. As the material to be joined, a substrate, a semiconductor element, or the like can be used independently of each other. As a specific embodiment, for example, it can be used as a bonding agent for surface mounting an electronic device on a printed wiring board or as a material for filling vias in a printed wiring board. Further, it can be used for forming a wiring circuit of a printed wiring board or forming an electrode of a chip component.
 以上、本発明をその好ましい実施形態に基づき説明したが、本発明は前記実施形態に制限されない。例えば、湿式還元法によって得られた銅粒子は、本発明の効果が奏される限りにおいて、得られた銅粒子が他の元素を不可避的に微量含むことや、銅粒子表面が不可避的に微量酸化されたりすることを排除するものではない。 Although the present invention has been described above based on the preferred embodiment, the present invention is not limited to the above embodiment. For example, in the copper particles obtained by the wet reduction method, as long as the effect of the present invention is exhibited, the obtained copper particles inevitably contain a trace amount of other elements, and the surface of the copper particles is inevitably a trace amount. It does not exclude being oxidized.
 以下、実施例により本発明を更に詳細に説明する。しかしながら本発明の範囲は、かかる実施例に制限されない。 Hereinafter, the present invention will be described in more detail with reference to Examples. However, the scope of the present invention is not limited to such examples.
〔実施例1〕
 本実施例は、いずれの工程も有機高分子の非存在下で接合用組成物を製造した。
(1)湿式還元法による銅粒子の生成
 36リットルのステンレス製タンク中に、第1液媒として温純水5.0リットル及びメタノール5.0リットルの混合液媒と、銅源として2.5kgの酢酸銅とを入れて、液温40℃で30分間撹拌して酢酸銅を溶解させた。次いで、150gのヒドラジンを液媒中に一括添加した後、液温40℃で30分間撹拌を継続し、液媒中に亜酸化銅の粒子を生成させた。30分経過後、更に1400gのヒドラジンを液媒中に一括添加した後、液温40℃で60分間撹拌を継続し、亜酸化銅の微粒子を金属銅の微粒子に還元した。このようにして、銅粒子が第1液媒に分散した分散体を得た。この分散体は湿潤状態を維持していた。得られた銅粒子の粒径DSEM50は、155nmであった。
[Example 1]
In this example, a bonding composition was produced in the absence of an organic polymer in each step.
(1) Generation of Copper Particles by Wet Reduction Method In a 36 liter stainless steel tank, a mixed liquid medium of 5.0 liters of warm pure water and 5.0 liters of methanol as the first liquid medium and 2.5 kg of acetic acid as the copper source. Copper was added and stirred at a liquid temperature of 40 ° C. for 30 minutes to dissolve copper acetate. Next, 150 g of hydrazine was added all at once to the liquid medium, and then stirring was continued at a liquid temperature of 40 ° C. for 30 minutes to generate copper oxide particles in the liquid medium. After 30 minutes had passed, 1400 g of hydrazine was added to the liquid medium all at once, and then stirring was continued at a liquid temperature of 40 ° C. for 60 minutes to reduce the fine particles of cuprous oxide into fine particles of metallic copper. In this way, a dispersion in which the copper particles were dispersed in the first liquid medium was obtained. This dispersion remained moist. The particle size D SEM50 of the obtained copper particles was 155 nm.
(2)液媒の置換
 本実施例では、第1液媒から他の液媒への置換を複数回行い、その後、最終の置換として第2液媒への置換を行った。すべての工程は、分散体の湿潤状態を維持した状態で行った。
 詳細には、第1の他の液媒として、第1液媒に相溶可能な純水を用いた。銅粒子の第1液媒分散体をデカンテーション法によって、電導度が3.5mSになるまで純水で洗浄処理し、銅粒子が水に分散した第1分散体を得た。この第1分散体は湿潤状態を維持していた。
 次いで、第2の他の液媒として、第1の他の液媒に相溶可能な変性アルコール(エタノール89質量%と2-プロパノール11質量%との混合液媒)を用いた。第1分散体中の水分濃度が1質量%以下になるまでロータリーフィルターにて変性アルコールで洗浄処理し、銅粒子が変性アルコールに分散した第2分散体を得た。この第2分散体は湿潤状態を維持していた。
 続いて、最終の置換に用いる第2液媒として、第2の他の液媒に相溶可能なヘキシレングリコールを用いた。第2分散体中の変性アルコール濃度が3質量%以下になるまでロータリーフィルターにてヘキシレングリコールで洗浄処理した後、加圧ろ過によりヘキシレングリコールを固液分離し、銅粒子が第2液媒に分散した接合用組成物を得た。この接合用組成物は固形分濃度が92%の湿潤状態を維持していた。
(2) Substitution of liquid medium In this example, the first liquid medium was replaced with another liquid medium a plurality of times, and then the second liquid medium was replaced as the final replacement. All steps were carried out while maintaining the wet state of the dispersion.
Specifically, as the first other liquid medium, pure water compatible with the first liquid medium was used. The first liquid medium dispersion of copper particles was washed with pure water until the conductivity became 3.5 mS by a decantation method to obtain a first dispersion in which copper particles were dispersed in water. The first dispersion remained moist.
Next, as the second other liquid medium, a modified alcohol (a mixed liquid medium of 89% by mass of ethanol and 11% by mass of 2-propanol) compatible with the first other liquid medium was used. The first dispersion was washed with a modified alcohol with a rotary filter until the water concentration in the first dispersion became 1% by mass or less to obtain a second dispersion in which copper particles were dispersed in the modified alcohol. This second dispersion remained moist.
Subsequently, as the second liquid medium used for the final substitution, hexylene glycol compatible with the second other liquid medium was used. After washing with hexylene glycol with a rotary filter until the modified alcohol concentration in the second dispersion becomes 3% by mass or less, hexylene glycol is solid-liquid separated by pressure filtration, and copper particles are used as the second liquid medium. A bonding composition dispersed in the above was obtained. This bonding composition maintained a wet state with a solid content concentration of 92%.
(3)接合用ペーストの調製
 接合用組成物を7.6質量部、接合用組成物に含まれる銅粒子以外の金属粒子(銅粒子、1200YF、三井金属鉱業株式会社製)を3質量部、固形分濃度が50質量%のBIS-TRIS/ヘキシレングリコール溶液を0.5質量部、及びポリエチレングリコール300を0.1質量部混合し、残部としてヘキシレングリコールを用いて、銅粒子の濃度が76質量%となるように、銅粒子を含む接合用ペーストを調製した。
(3) Preparation of bonding paste 7.6 parts by mass of the bonding composition, 3 parts by mass of metal particles (copper particles, 1200YF, manufactured by Mitsui Metal Mining Co., Ltd.) other than copper particles contained in the bonding composition. 0.5 parts by mass of BIS-TRIS / hexylene glycol solution having a solid content concentration of 50% by mass and 0.1 parts by mass of polyethylene glycol 300 were mixed, and hexylene glycol was used as the balance to adjust the concentration of copper particles. A bonding paste containing copper particles was prepared so as to have a mass content of 76% by mass.
〔比較例1〕
 実施例1と同様に(1)湿式還元法による銅粒子の生成を行った後、銅粒子の第1液媒分散体をデカンテーション法によって、電導度が3mSになるまで純水で洗浄処理し、銅粒子が水に分散した分散体を得た。この分散体は湿潤状態を維持していた。
 次いで、分散体を50℃まで加温し、撹拌しながら、銅粒子含有量に対するジメチルグリオキシム含有量が0.5質量%となるように、ジメチルグリオキシム/メタノール溶液を添加し、液温50℃で1時間撹拌し、表面処理された銅粒子の水/メタノール分散体を得た。
 その後、表面処理済み銅粒子を真空乾燥し、乾燥状態の銅粒子を得た。この銅粒子には、液媒は存在していない。
 最後に、接合用組成物に代えて、乾燥状態の銅粒子を用いて、実施例1と同様の組成及び濃度の接合用ペーストを調製した。
[Comparative Example 1]
Similar to Example 1, (1) after the copper particles were generated by the wet reduction method, the first liquid medium dispersion of the copper particles was washed with pure water by the decantation method until the conductivity became 3 mS. , Obtained a dispersion in which copper particles were dispersed in water. This dispersion remained moist.
Next, the dispersion was heated to 50 ° C., and while stirring, a dimethylglyoxime / methanol solution was added so that the dimethylglyoxime content was 0.5% by mass with respect to the copper particle content, and the liquid temperature was 50. The mixture was stirred at ° C. for 1 hour to obtain a water / methanol dispersion of surface-treated copper particles.
Then, the surface-treated copper particles were vacuum-dried to obtain dried copper particles. There is no liquid medium in these copper particles.
Finally, instead of the bonding composition, dried copper particles were used to prepare a bonding paste having the same composition and concentration as in Example 1.
〔密着性の評価〕
 実施例及び比較例の接合用ペーストを、縦10mm×横10mm×厚み110μmの寸法で、銅板(縦20mm×横20mm×厚み2mm)の表面中央部にスクリーン印刷し、接合用ペーストを110℃で20分間乾燥させて、乾燥膜を得た。
 次に、表面がAgメッキされたアルミナ板(縦5mm×横5mm×厚み0.5mm)を乾燥膜上に載せ、窒素雰囲気下で6MPa、昇温速度120℃/分で280℃、20分間焼結させて、銅板とアルミナ板とを接合させた。
 接合後、超音波探傷装置(日立パワーソリューションズ社製、型番:FineSATIII)で75MHzのプローブを用いて、反射法により、銅板におけるアルミナ板が配されている面側から観察し、乾燥膜の焼結体中のボイドの有無と、乾燥膜の焼結体におけるアルミナ板の外周部(加圧されていない領域)の状態とを観察した。密な焼結構造であるほど色が濃く観察される。結果を図1に示す。
[Evaluation of adhesion]
The bonding pastes of Examples and Comparative Examples are screen-printed on the center surface of a copper plate (length 20 mm x width 20 mm x thickness 2 mm) with dimensions of 10 mm in length × 10 mm in width × 110 μm in thickness, and the paste for bonding is printed at 110 ° C. It was dried for 20 minutes to obtain a dry film.
Next, an alumina plate (length 5 mm × width 5 mm × thickness 0.5 mm) whose surface is Ag-plated is placed on a dry film and baked at 6 MPa in a nitrogen atmosphere at a heating rate of 120 ° C./min at 280 ° C. for 20 minutes. The copper plate and the alumina plate were joined together.
After joining, use an ultrasonic flaw detector (manufactured by Hitachi Power Solutions, model number: FineSATIII) with a 75 MHz probe to observe from the surface side of the copper plate where the alumina plate is arranged by the reflection method, and sinter the dry film. The presence or absence of voids in the body and the state of the outer peripheral portion (non-pressurized region) of the alumina plate in the sintered body of the dried film were observed. The denser the sintered structure, the darker the color is observed. The results are shown in FIG.
 図1中、アルミナ板が配置されている領域を符号Aとし、乾燥膜の焼結体の存在領域を符号Bとし、銅板が露出している領域を符号Cとして示す。
 図1(a)に示すように、実施例1の接合用組成物を用いて得られたペーストの焼結体は、アルミナ板が配置されている領域Aは色が濃く観察されているので、ボイドが少ない緻密な構造が形成され、アルミナ板と銅板との接合状態が良好であることが判る。また、アルミナ板の外周に位置する焼結体の存在領域Bでは、観察される色が均一であり、該焼結体と銅板との剥離が観察されなかった。したがって、実施例1の接合用組成物を用いたペーストは、他の部材との密着性に優れることが判る。
In FIG. 1, the region where the alumina plate is arranged is indicated by reference numeral A, the region where the sintered body of the dried film exists is indicated by reference numeral B, and the region where the copper plate is exposed is indicated by reference numeral C.
As shown in FIG. 1A, in the sintered body of the paste obtained by using the bonding composition of Example 1, the region A in which the alumina plate is arranged is observed to be dark in color. It can be seen that a dense structure with few voids is formed and the bonding state between the alumina plate and the copper plate is good. Further, in the region B where the sintered body is located on the outer periphery of the alumina plate, the observed color was uniform, and peeling between the sintered body and the copper plate was not observed. Therefore, it can be seen that the paste using the bonding composition of Example 1 is excellent in adhesion to other members.
 一方、図1(b)に示すように、比較例1の接合用組成物を用いて得られたペーストの焼結体は、アルミナ板が配置されている領域Aは色が濃く観察されているので、アルミナ板と銅板との接合状態が良好であることが判るが、アルミナ板の外周に位置する焼結体の存在領域Bでは、観察される色が不均一であり、該焼結体と銅板との剥離が多く観察された。したがって、比較例1の接合用組成物を用いたペーストは、他の部材との密着性に劣ることが判る。 On the other hand, as shown in FIG. 1 (b), in the sintered body of the paste obtained by using the bonding composition of Comparative Example 1, the region A in which the alumina plate is arranged is observed to be dark in color. Therefore, it can be seen that the bonding state between the alumina plate and the copper plate is good, but in the region B where the sintered body is located on the outer periphery of the alumina plate, the observed color is non-uniform, and the sintered body and the sintered body are in a non-uniform state. Many peelings from the copper plate were observed. Therefore, it can be seen that the paste using the bonding composition of Comparative Example 1 is inferior in adhesion to other members.
 本発明の製造方法によれば、焼結時において、他の部材との密着性に優れる接合用組成物を得ることができる。
 
According to the production method of the present invention, it is possible to obtain a bonding composition having excellent adhesion to other members at the time of sintering.

Claims (9)

  1.  湿式還元法によって第1液媒中に銅粒子を生成させて、該銅粒子の分散体を調製し、然る後に、
     前記分散体の湿潤状態を維持しながら、該分散体の第1液媒を最終的に第2液媒に置換して、前記銅粒子と第2液媒とを含む接合用組成物を得る、接合用組成物の製造方法。
    Copper particles are generated in the first liquid medium by a wet reduction method to prepare a dispersion of the copper particles, and then after that,
    While maintaining the wet state of the dispersion, the first liquid medium of the dispersion is finally replaced with the second liquid medium to obtain a bonding composition containing the copper particles and the second liquid medium. A method for producing a bonding composition.
  2.  液媒の置換を100℃未満で行う、請求項1に記載の製造方法。 The production method according to claim 1, wherein the liquid medium is replaced at a temperature of less than 100 ° C.
  3.  第2液媒として、水、アルコール、ケトン、エステル、エーテル及び炭化水素のうち一種以上を用いる、請求項1又は2に記載の製造方法。 The production method according to claim 1 or 2, wherein one or more of water, alcohol, ketone, ester, ether and hydrocarbon is used as the second liquid medium.
  4.  前記銅粒子は、走査型電子顕微鏡によって測定された累積体積50容量%における体積累積粒径DSEM50が100nm以上300nm以下である、請求項1~3のいずれか一項に記載の製造方法。 The production method according to any one of claims 1 to 3, wherein the copper particles have a volume cumulative particle size D SEM50 of 100 nm or more and 300 nm or less in a cumulative volume of 50% by volume measured by a scanning electron microscope.
  5.  第1液媒を他の液媒に一回以上置換し、最終の置換に第2液媒を用いる、請求項1~4のいずれか一項に組成物の製造方法。 The method for producing a composition according to any one of claims 1 to 4, wherein the first liquid medium is replaced with another liquid medium at least once, and the second liquid medium is used for the final replacement.
  6.  前記分散体の湿潤状態を維持しながら、第1液媒を他の液媒に置換する、請求項5に記載の製造方法。 The production method according to claim 5, wherein the first liquid medium is replaced with another liquid medium while maintaining the wet state of the dispersion.
  7.  有機高分子の非存在下で行う、請求項1~6のいずれか一項に記載の製造方法。 The production method according to any one of claims 1 to 6, which is carried out in the absence of an organic polymer.
  8.  請求項1~7のいずれか一項に記載の製造方法で得られた接合用組成物を含む導電性ペーストの製造方法。 A method for producing a conductive paste containing a bonding composition obtained by the production method according to any one of claims 1 to 7.
  9.  請求項1~7のいずれか一項に記載の製造方法で得られた接合用組成物を2つの被接合材の間に配する、被接合材の接合方法。
     
    A method for joining a material to be joined, wherein the composition for joining obtained by the production method according to any one of claims 1 to 7 is arranged between two materials to be joined.
PCT/JP2021/010064 2020-03-27 2021-03-12 Method for producing bonding composition WO2021193144A1 (en)

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JP2003151381A (en) 2001-11-09 2003-05-23 Murata Mfg Co Ltd Manufacturing method of conductive paste and conductive paste
JP2003253301A (en) 2002-03-01 2003-09-10 Murata Mfg Co Ltd Method for manufacturing metal powder for conductive paste, metal powder for conductive paste, conductive paste, and multilayer ceramic electronic part
US20090146117A1 (en) 2004-11-29 2009-06-11 Dainippon Ink And Chemicals, Inc. Method for producing surface-treated silver-containing powder and silver paste using surface-treated silver-containing powder
JP2007224422A (en) 2007-03-12 2007-09-06 Dowa Holdings Co Ltd Silver powder and paste using the same
JP2015168878A (en) 2014-03-10 2015-09-28 三井金属鉱業株式会社 copper powder
WO2017057301A1 (en) * 2015-09-30 2017-04-06 住友電気工業株式会社 Coating liquid for forming electroconductive layer, and method for manufacturing electroconductive layer

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